Page 246 - Design and Operation of Heat Exchangers and their Networks
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236   Design and operation of heat exchangers and their networks


          or in a matrix form:

                                         0
                                    0
                                           0
                                   T ¼ G T + GT  00                   (6.19)
                                    E            E
                                   00   000  0  00  00
                                 T ¼ G T + G T E                      (6.20)
                                  T                       T
                  0    0  0    0          00  00  00   00
                     ½
          where T ¼ t t ⋯ t Š and T ¼ t ½     1  t 2  ⋯ t N 00 Š are the entrance
                         2
                       1
                               N
                                 0
          and exit stream temperatures of the network, respectively.
             As has been shown in Section 3.6, substituting Eq. (6.13) into
          Eqs. (6.19), (6.20), we can explicitly express the inlet and outlet fluid tem-
          peratures of individual heat exchangers and the exit stream temperatures of
          the network with Eqs. (6.21), (6.13), (6.22), respectively.
                                  0            1  0  0
                                 T ¼ I GVð   Þ G T                    (6.21)
                                  E
                                                         1
                                             00
                                        000
                        000
                                  00
                               00
                           0
                                                           0
                   00
                 T ¼ G T + G T ¼ G + G VI GVÞ G T             0       (6.22)
                                                ð
                                  E
             Because Eqs. (6.21), (6.22) contain the calculation of an N N inverse
          matrix, for a large heat exchanger network, more computing time might be
          required. As an alternative, the “upwind” iterative calculation method is
          recommended. The convergence of the iteration is ensured by alternately
          recalculating the temperatures of the hot/cold process streams with fixed
          cold/hot stream temperatures.
          (1) At the beginning, set all unknown inlet and outlet temperatures of the
              hot and cold process streams equal to their supply temperatures of the
              network.
          (2) Starting from the network entrances of the hot process streams and
              along the stream flow direction, calculate the outlet temperature of
              hot stream in each heat exchanger according to its known or assumed
              inlet temperature of the hot and cold streams but do not calculate the
              outlet temperature of the cold stream.
          (3) Starting from the network entrances of the cold process streams and
              along the stream flow direction, calculate the outlet temperature of cold
              stream in each heat exchanger according to its known or calculated inlet
              temperature of the hot and cold streams but do not calculate the outlet
              temperature of the hot stream.
          (4) Repeat Steps (2) and (3) to correct the outlet temperatures of hot and
              cold streams, respectively, until the given accuracy is achieved.
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